WO2000014039A1 - Styrene monomer polymerization inhibition using substituted dihydroxyarenes and nitroxides - Google Patents

Styrene monomer polymerization inhibition using substituted dihydroxyarenes and nitroxides Download PDF

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Publication number
WO2000014039A1
WO2000014039A1 PCT/US1999/020529 US9920529W WO0014039A1 WO 2000014039 A1 WO2000014039 A1 WO 2000014039A1 US 9920529 W US9920529 W US 9920529W WO 0014039 A1 WO0014039 A1 WO 0014039A1
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WO
WIPO (PCT)
Prior art keywords
composition
group
hydrogen
vinyl aromatic
carbon atoms
Prior art date
Application number
PCT/US1999/020529
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English (en)
French (fr)
Inventor
Muslim Shahid
Original Assignee
Baker Hughes Incorporated
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Baker Hughes Incorporated filed Critical Baker Hughes Incorporated
Priority to AT99944100T priority Critical patent/ATE230714T1/de
Priority to JP2000568799A priority patent/JP2002524430A/ja
Priority to EP99944100A priority patent/EP1119533B1/en
Priority to DE69904848T priority patent/DE69904848T2/de
Priority to AU57059/99A priority patent/AU760809B2/en
Priority to BR9913523-0A priority patent/BR9913523A/pt
Priority to KR1020017003033A priority patent/KR20010079775A/ko
Priority to CA002342945A priority patent/CA2342945A1/en
Publication of WO2000014039A1 publication Critical patent/WO2000014039A1/en
Priority to NO20011017A priority patent/NO20011017L/no

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K15/00Anti-oxidant compositions; Compositions inhibiting chemical change
    • C09K15/04Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds
    • C09K15/30Anti-oxidant compositions; Compositions inhibiting chemical change containing organic compounds containing heterocyclic ring with at least one nitrogen atom as ring member
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C7/00Purification; Separation; Use of additives
    • C07C7/20Use of additives, e.g. for stabilisation

Definitions

  • the present invention relates to methods and compositions for inhibiting the polymerization of vinyl monomers, and more particularly relates, in one embodiment, to methods and compositions for inhibiting the polymerization of vinyl aromatic monomers.
  • Still another object of the invention is to permit use of a composition to effectively inhibit the polymerization of styrene that has little or no environmental concerns.
  • a composition for inhibiting polymerization of vinyl aromatic compounds that includes a dihydroxyarene, a hydrogen transfer agent, and a stable nitroxide.
  • a dihydroxyarene or a substituted alkyl-dihydroxyarene, a hydrogen transfer agent, and a stable nitroxide is an effective treatment to control styrene monomer polymerization. This treatment protocol is most effective when formulated in an organic amine, although the composition may find effective use without the organic amine.
  • suitable vinyl aromatic monomers that may be polymerization inhibited by the compositions and methods of this invention include, but are not necessarily limited to styrene, substituted styrene, divinylbenzene, vinyltoluene, vinyl naphthalene, polyvinylbenzenes, and isomers thereof.
  • the aromatic monomer is styrene. It is anticipated that this invention could also inhibit the polymerization of non- aromatic vinyl compounds, e.g. acrylonitrile, vinyl chloride, acrylic acid and the like.
  • Suitable substituted alkyl-dihydroxyarenes for the polymerization inhibiting composition of the invention may include, but are not necessarily limited to, substituted alkyl-dihydroxybenzenes having the formula:
  • R 1 and R 2 are the same or different and are independently selected from the group consisting of hydrogen, straight, branched, and cyclic alkyl groups averaging from about 1 to about 6 carbon atoms, preferably from about 1 to about 4 carbon atoms, and where x averages from about 0 to about 9, and preferably in one embodiment from about 1 to about 9. In one preferred embodiment, both R 1 and R 2 are not simultaneously hydrogen.
  • Examples of specific substituted alkyl-dihydroxyarenes that would be suitable in the composition of this invention include, but are not necessarily limited to, hydroquinone; tert-butylhydroquinone; 2,5-di-tert-butylhydroquinone; tert-butylcatechol; hydroquinone; 3,5-di-tert-butylcatechol; catechol; 3,33 ⁇ 3'-tetramefhyl-l ,r-spiro-bj ' s- indane-5,5',6,6'-teterol; and mixtures thereof.
  • Hydrogen Transfer Agent suitable for use in the polymerization inhibiting composition of this invention include, but are not necessarily limited to, naphthalene; anthracene; decalin; hydroquinoline; 1,23,4-tetrahydronaphthalene (TETRALIN ® ; DuPont); 9,10-dihydroanthracene; fluorene; squalane; squalene; tetramethylhydroquinoline; and mixtures thereof.
  • TETRALIN ® 1,23,4-tetrahydronaphthalene
  • the stable nitroxide of the composition useful for inhibiting polymerization of vinyl aromatic compounds may include, but are not necessarily limited to those having the formula:
  • R 3 , R 4 , R 5 , and R 6 are the same or different and are independently selected from the group consisting of straight, branched, or cyclic alkyl groups of from 1 to about 9 carbon atoms, preferably from about 1 to 3 carbon atoms; where Z is selected from the group consisting of hydrogen, oxygen, alkyl groups, alkoxy groups, hydroxyl, aryl groups, alkaryl groups, heterocyclic alkyl groups; and where when Z contains carbon atoms, may contain an average of from about 1 to 9 carbon atoms, preferably from about 1 to 3 carbon atoms.
  • R 3 and R 4 may be joined together to form a cyclic moiety which may be alkylene or aralkylene. The same is true for the R 5 and R 6 pair.
  • stable nitroxides examples include, but are not necessarily limited to, 2,2,6,6-tetramethyl-l- piperidinyloxyl (TEMPO); 4-OXO TEMPO; l-oxyl-2,2,6,6-tetramethylpiperidine; 1- oxyl-2,2,6,6-tetramethylpiperidin-4-one; l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl-2- acetate; l-oxyl-2,2,6,6-tetramethyl-l-piperidin-4-yl-2-ethylhexanoate and mixtures thereof.
  • the stable nitroxides may include, but are not necessarily limited to those having the formula:
  • R 9 R 10 R n )C [(R 9 R 10 R n )C] 2 N-O * where R°, R 10 , and R 1 ' are independently selected from the group consisting of hydrogen, straight, branched or cyclic alkyl, aryl, aralkyl, and alkaryl moieties; where only one of R 9 , R 10 , and R 1 ' on each C can be hydrogen at a time; where one or more of R 9 , R 10 , and R 1 ' on one C may be joined to a R 9 , R 10 , and R 1 ' on the other C to form a cyclic moiety selected from the group consisting of alkylene, and aralkylene moieties; where any two of the R 9 , R 10 , and R 1 ' on any one C may be joined together to form a cycloalkyl; where any of the above definitions of R 9 , R 10 , and R 1 ' may contain one or more heteroatoms selected from the
  • Organic amines suitable in the methods and compositions of this invention may include, but are not necessarily limited to, organic amines of the formula:
  • R 7 -NH-R 8 where R 7 and R 8 are the same or different and are independently selected from the group consisting of hydrogen; straight, branched, and cyclic alkyl groups; alkoxy groups; hydroxyalkyl groups; and aminoalkyl groups; averaging of from about 1 to about 20 carbon atoms, preferably from about 6 to about 9 carbon atoms, where both R 7 and R 8 are not simultaneously hydrogen.
  • Examples of specific organic amines that would be suitable in the composition of this invention include, but are not necessarily limited to, butylamine; hexylamine; n- octylamine; dodecylamine; cyclohexylamine; N,N-dihexylamine; ethanolamine; N-(2- aminoethyl)ethanol; ethylenediamine; 2-aminopropanol; and mixtures thereof.
  • the composition of this invention may have from about 1 to about 10,000 ppm of the alkyl-dihydroxyarene; from about 1 to about 10,000 ppm of the hydrogen transfer agent; and from about 1 to about 10,000 ppm of the stable nitroxide, based on the total amount of vinyl aromatic compound being treated.
  • the proportions range from about 34 to about 200 ppm of the alkyl- dihydroxyarene; from about 34 to about 118 ppm of the hydrogen transfer agent; and from about 34 to about 145 ppm of the stable nitroxide, based on the total amount of vinyl aromatic compound being treated.
  • the composition of this invention may have from about 1 to about 10,000 ppm of the alkyl-dihydroxyarene; from about 1 to about 10,000 ppm of the hydrogen transfer agent; from 1 to about 10,000 ppm of the stable nitroxide and from about 1 to about 10,000 ppm of the organic amine, based on the total amount of vinyl aromatic compound being treated.
  • the proportions range from about 34 to about 200 ppm of the alkyl-dihydroxyarene; from about 34 to about 118 ppm of the hydrogen transfer agent; from about 34 to about 145 ppm of the stable nitroxide and from about 5 to about 300 ppm of the organic amine, based on the total amount of vinyl aromatic compound being treated.
  • the components of the composition may be simply mixed together. They may be mixed together in a single composition prior to addition to the vinyl aromatic compound, although they may also be added to the vinyl compound separately.
  • Inhibited styrene monomer purchased from Aldrich Chemicals was distilled under vacuum (45°C, 29 mm Hg) to remove the conventional storage inhibitor 4-tert-butyl- pyrocatechol. The distilled styrene was checked for polymer content by sampling a portion and mixing in cold methanol. The distillation of the styrene monomer is considered successful if the two liquids mix completely with no presence of haze or cloudy appearance. One hundred mis of distilled styrene was transferred into a 250 ml, three-necked, round bottom reaction flask. The desired amount of inhibitors) were added to the distilled styrene monomer.
  • the reaction flask was also equipped with a condenser, a thermocouple (type J), thermometer (Celsius), and a gas sparge tube.
  • the reaction apparatus was placed in an oil bath. The temperature of the oil bath could be raised by the use of an external heating device.
  • the styrene monomer was purged with nitrogen for 20 minutes to insure that the effect of oxygen on styrene monomer and/or inhibitors would be insignificant during the test run. While continuing the nitrogen purge, the temperature of the oil bath and subsequently, the styrene/inhibitor(s) composition was raised until a styrene monomer/inhibitor(s) composition temperature of 118°C ⁇ 2°C was obtained.
  • the styrene monomer/inhibitor(s) composition was maintained under these conditions for 90 minutes.
  • the reaction flask apparatus was removed from the hot oil bath and the styrene monomer/inhibitor(s) composition was allowed to cool to ambient under continuing nitrogen purge.
  • the styrene monomer/inhibitor(s) composition was transferred from the reaction flask into a 1000 ml beaker containing 200 ml of cold methanol.
  • the styrene/methanol mixture was mixed until the polymer, if any, agglomerates. Eight hundred ml of n-heptane was added to the styrene methanol composition.
  • the polystyrene if any, was allowed to settle out of solution until the liquid phase of the composition was clear.
  • the styrene/methanol/n- heptane/polymer mixture was filtered through a 1.0 ⁇ m glass fiber filter. Any remaining polymer was washed from the beaker with n-heptane through the glass fiber filter paper.
  • the filter paper was placed into an oven with ventilation capable of maintaining a temperature of 150°C ⁇ 2°C for 16 hours.
  • the dried polymer was cooled in a desiccator, and the weight of the polymer was obtained by taking the difference of the weight of filter paper/polymer minus the initial weight of filter paper. Results were reported as percent polymer formed by weight of polymer formed in mgs divided by the weight of the original styrene monomer used in mg multiplied by 100.
  • Uninhibited styrene monomer prepared by the above procedure stored at -25°F (- 13°C) was used to evaluate the additives of the instant invention, as described below. As noted, a 90 minute nitrogen reflux test method was used to generate the data. Table I summaries the results from the initial testing.
  • test apparatus is equipped with a septum and a 5 ml sample is extracted with a syringe at designated time intervals.
  • Example 32 The data below summarizes the amount of polymer formed during the duration of the test when using the combination of inhibitors: 52 ppm TETRALIN, 87 ppm 2,5-di- tert-butyl HQ, and 65 ppm 4-OH TEMPO formulated in n-octylamine. Samples were extracted as in Example 31.
  • Table VII shows that even when the di-hydroxyarene compound is not formulated in an organic amine the combinations of stable free radical, hydrogen transfer agent and di-hydroxyarene materials are still quite effective.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Water Supply & Treatment (AREA)
  • Materials Engineering (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Polymerisation Methods In General (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
PCT/US1999/020529 1998-09-09 1999-09-08 Styrene monomer polymerization inhibition using substituted dihydroxyarenes and nitroxides WO2000014039A1 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
AT99944100T ATE230714T1 (de) 1998-09-09 1999-09-08 Inhibierung der polymerisation von styrolmonomeren mit substituierten dihydroxyarenen und stickoxiden
JP2000568799A JP2002524430A (ja) 1998-09-09 1999-09-08 置換ジヒドロキシアレーンとニトロキシドとを使用したスチレンモノマー重合禁止
EP99944100A EP1119533B1 (en) 1998-09-09 1999-09-08 Styrene monomer polymerization inhibition using substituted dihydroxyarenes and nitroxides
DE69904848T DE69904848T2 (de) 1998-09-09 1999-09-08 Inhibierung der polymerisation von styrolmonomeren mit substituierten dihydroxyarenen und stickoxiden
AU57059/99A AU760809B2 (en) 1998-09-09 1999-09-08 Styrene monomer polymerization inhibition using substituted dihydroxyarenes and nitroxides
BR9913523-0A BR9913523A (pt) 1998-09-09 1999-09-08 Inibição de polimerização de monÈmero estireno utilizando dihidroxiarenos e nitróxidos substituìdos
KR1020017003033A KR20010079775A (ko) 1998-09-09 1999-09-08 치환 디히드록시아렌 및 니트록시드를 이용한 스티렌모노머 중합반응 억제방법
CA002342945A CA2342945A1 (en) 1998-09-09 1999-09-08 Styrene monomer polymerization inhibition using substituted dihydroxyarenes and nitroxides
NO20011017A NO20011017L (no) 1998-09-09 2001-02-27 Polymeriserings-inhibitering av styren-monomerer

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US15048898A 1998-09-09 1998-09-09
US09/150,488 1998-09-09

Publications (1)

Publication Number Publication Date
WO2000014039A1 true WO2000014039A1 (en) 2000-03-16

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US (1) US6284936B2 (ko)
EP (1) EP1119533B1 (ko)
JP (1) JP2002524430A (ko)
KR (1) KR20010079775A (ko)
AT (1) ATE230714T1 (ko)
AU (1) AU760809B2 (ko)
BR (1) BR9913523A (ko)
CA (1) CA2342945A1 (ko)
DE (1) DE69904848T2 (ko)
ES (1) ES2190657T3 (ko)
NO (1) NO20011017L (ko)
TW (1) TW544447B (ko)
WO (1) WO2000014039A1 (ko)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001040404A1 (en) * 1999-12-03 2001-06-07 Uniroyal Chemical Company, Inc. Composition and method for inhibiting polymerization and polymer growth
WO2001040149A2 (en) * 1999-12-02 2001-06-07 Crompton Corporation Inhibition of polymerization of unsaturated monomers
JP2004526796A (ja) * 2001-04-30 2004-09-02 ベイカー ヒューズ インコーポレイテッド ポプコーンポリマーの成長阻止
JP2004527632A (ja) * 2001-05-22 2004-09-09 ジーイー・ベッツ・インコーポレイテッド ビニルモノマーの重合を抑制する方法及び組成物
WO2023161222A1 (en) 2022-02-23 2023-08-31 Totalenergies Onetech Cleaning process of a vinyl aromatic compounds distillation unit and processes including such cleaning process

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US6761833B2 (en) * 2001-03-20 2004-07-13 Atofina Chemicals, Inc. Stabilization of monomers by compositions based on alkylhydroxylamines
AU2005247328B2 (en) * 2004-05-03 2011-03-10 Shalon Ventures, L.P. Polycationic antimicrobial therapeutic
JP5675184B2 (ja) * 2010-06-18 2015-02-25 伯東株式会社 ビニル化合物の重合防止剤組成物ならびにこれを用いたビニル化合物の重合防止方法
KR101532990B1 (ko) * 2011-09-22 2015-07-01 도요 고무 고교 가부시키가이샤 연마 패드
CA2857384C (en) * 2011-11-29 2016-08-16 Dorf Ketal Chemicals (India) Private Limited Amine based additive composition for control and inhibition of polymerization of styrene, and method of use thereof
RU2625300C2 (ru) * 2011-12-02 2017-07-13 Дорф Кетал Кемикалс (Индия) Прайвит Лимитэд Композиция добавки на основе амина и нитроксида для контроля и ингибирования полимеризации стирола и способ ее использования
US9611336B2 (en) 2012-10-25 2017-04-04 Baker Hughes Incorporated Quinone compounds for inhibiting monomer polymerization
US9944577B2 (en) * 2012-10-25 2018-04-17 Baker Hughes, A Ge Company, Llc Hydroquinone compounds for inhibiting monomer polymerization
JP6503059B2 (ja) 2014-10-14 2019-04-17 エコラブ ユーエスエイ インク アクリレート/メタクリレートプロセスにおけるポリマーの汚損および凝集の低減
ES2912329T3 (es) 2015-03-18 2022-05-25 Ecolab Usa Inc El uso de compuestos de hidroxilamina lipófilos estables para inhibir la polimerización de monómeros de vinilo
US9957209B2 (en) 2015-03-31 2018-05-01 Ecolab Usa Inc. Use of quinone methides as antipolymerants for vinylic monomers
US10155705B2 (en) 2015-04-20 2018-12-18 Ecolab Usa Inc. Sterically hindered hydroquinones as antifoulants for unsaturated monomers
US20170158621A1 (en) * 2015-12-04 2017-06-08 Baker Hughes Incorporated Substituted phenol derivatives for mitigating fouling

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Cited By (7)

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Publication number Priority date Publication date Assignee Title
WO2001040149A2 (en) * 1999-12-02 2001-06-07 Crompton Corporation Inhibition of polymerization of unsaturated monomers
WO2001040149A3 (en) * 1999-12-02 2002-01-24 Crompton Corp Inhibition of polymerization of unsaturated monomers
US6653414B2 (en) 1999-12-02 2003-11-25 Uniroyal Chemical Company, Inc. Inhibition of polymerization of unsaturated monomers
WO2001040404A1 (en) * 1999-12-03 2001-06-07 Uniroyal Chemical Company, Inc. Composition and method for inhibiting polymerization and polymer growth
JP2004526796A (ja) * 2001-04-30 2004-09-02 ベイカー ヒューズ インコーポレイテッド ポプコーンポリマーの成長阻止
JP2004527632A (ja) * 2001-05-22 2004-09-09 ジーイー・ベッツ・インコーポレイテッド ビニルモノマーの重合を抑制する方法及び組成物
WO2023161222A1 (en) 2022-02-23 2023-08-31 Totalenergies Onetech Cleaning process of a vinyl aromatic compounds distillation unit and processes including such cleaning process

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US6284936B2 (en) 2001-09-04
DE69904848D1 (de) 2003-02-13
ATE230714T1 (de) 2003-01-15
AU760809B2 (en) 2003-05-22
ES2190657T3 (es) 2003-08-01
NO20011017L (no) 2001-04-23
BR9913523A (pt) 2001-06-05
US20010003360A1 (en) 2001-06-14
CA2342945A1 (en) 2000-03-16
EP1119533B1 (en) 2003-01-08
EP1119533A1 (en) 2001-08-01
TW544447B (en) 2003-08-01
NO20011017D0 (no) 2001-02-27
KR20010079775A (ko) 2001-08-22
AU5705999A (en) 2000-03-27
JP2002524430A (ja) 2002-08-06
DE69904848T2 (de) 2003-11-06

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